“…Simulation results were obtained for the variation of mean air temperature (T m ) and sensible Nusselt number (Nu s ) along the axial direction of the channel and the comparison results are shown in Figures 3(a) and (b), respectively. As can be seen from the above figures, the results predicted by the present numerical algorithm are in close agreement with the results of Hammou et al [13] obtained using velocity-pressure equations and SIMPLER algorithm.…”
Section: Mesh Sensitivity and Validation Resultssupporting
confidence: 91%
“…Our predicted results for the reattachment length and the local maximum Nusselt number are in close agreement with the above references. For the purpose of comparing our results for double diffusive mixed convection in a channel, the evaporation problem discussed by Hammou et al [13] has been considered. Simulation results were obtained for the variation of mean air temperature (T m ) and sensible Nusselt number (Nu s ) along the axial direction of the channel and the comparison results are shown in Figures 3(a) and (b), respectively.…”
Section: Mesh Sensitivity and Validation Resultsmentioning
confidence: 99%
“…The combined effect of thermal and solutal buoyancy forces in vertical parallel plates has received a considerable attention in evaporation and condensation applications. Hammou et al [13] studied the effect of buoyancy ratio and Richardson number on simultaneous convective heat and mass transfer during flow of humid air in a vertical channel with isothermal wet walls. Brown and Lai [14] studied the combined effect of heat and mass transfer in 165 a horizontal channel with open cavity and focused on the development of correlations for Nusselt and Sherwood numbers.…”
SUMMARYThis paper presents results on the combined effect of thermo-solutal buoyancy forces on the recirculatory flow behavior in a horizontal channel with backward-facing step and the ensuing impact on heat and mass transfer phenomena. The governing equations for double diffusive mixed convection are represented in velocity-vorticity form of momentum equations, velocity Poisson equations, energy and concentration equations. Galerkin's finite-element method has been employed to solve the governing equations. Recirculatory flow fields with heat and mass transfer are simulated for opposing and aiding thermo-solutal buoyancy forces by assuming suitable boundary conditions for energy and concentration equations. The effect of Richardson number (0.1 Ri 10) and buoyancy ratio (−10 N 10) on the recirculation bubble and Nusselt and Sherwood numbers are studied in detail. For Richardson number greater than unity, distinct variations in the gradients of Nusselt number and Sherwood number with buoyancy ratio are observed for flow regimes with opposing and aiding buoyancy forces.
“…Simulation results were obtained for the variation of mean air temperature (T m ) and sensible Nusselt number (Nu s ) along the axial direction of the channel and the comparison results are shown in Figures 3(a) and (b), respectively. As can be seen from the above figures, the results predicted by the present numerical algorithm are in close agreement with the results of Hammou et al [13] obtained using velocity-pressure equations and SIMPLER algorithm.…”
Section: Mesh Sensitivity and Validation Resultssupporting
confidence: 91%
“…Our predicted results for the reattachment length and the local maximum Nusselt number are in close agreement with the above references. For the purpose of comparing our results for double diffusive mixed convection in a channel, the evaporation problem discussed by Hammou et al [13] has been considered. Simulation results were obtained for the variation of mean air temperature (T m ) and sensible Nusselt number (Nu s ) along the axial direction of the channel and the comparison results are shown in Figures 3(a) and (b), respectively.…”
Section: Mesh Sensitivity and Validation Resultsmentioning
confidence: 99%
“…The combined effect of thermal and solutal buoyancy forces in vertical parallel plates has received a considerable attention in evaporation and condensation applications. Hammou et al [13] studied the effect of buoyancy ratio and Richardson number on simultaneous convective heat and mass transfer during flow of humid air in a vertical channel with isothermal wet walls. Brown and Lai [14] studied the combined effect of heat and mass transfer in 165 a horizontal channel with open cavity and focused on the development of correlations for Nusselt and Sherwood numbers.…”
SUMMARYThis paper presents results on the combined effect of thermo-solutal buoyancy forces on the recirculatory flow behavior in a horizontal channel with backward-facing step and the ensuing impact on heat and mass transfer phenomena. The governing equations for double diffusive mixed convection are represented in velocity-vorticity form of momentum equations, velocity Poisson equations, energy and concentration equations. Galerkin's finite-element method has been employed to solve the governing equations. Recirculatory flow fields with heat and mass transfer are simulated for opposing and aiding thermo-solutal buoyancy forces by assuming suitable boundary conditions for energy and concentration equations. The effect of Richardson number (0.1 Ri 10) and buoyancy ratio (−10 N 10) on the recirculation bubble and Nusselt and Sherwood numbers are studied in detail. For Richardson number greater than unity, distinct variations in the gradients of Nusselt number and Sherwood number with buoyancy ratio are observed for flow regimes with opposing and aiding buoyancy forces.
“…Furthermore, different grid sizes were considered to ensure that the solution was gridindependent. Results of the grid sensibility study are given by Ait Hammou et al (2004) and Kassim et al (2010). These results show that heat and mass transfer parameters, as well as the local variables, obtained for three grids 100x35, 200x70 and 400x140 vary within less than 5%.…”
“…Most of the studies in this category are concentrated on steady state laminar flow of Rayleigh number ranging from 10⁴ to 10⁶ [Desrayaud and Lauriat 2001, Hammou et al 2004and Laaroussi and Lauriat 2008. McBrain [1997], Catalin et al [2003] and Laguerre et al [2009] investigated temperature and mass concentration gradient induced laminar flow in an enclosure.…”
Section: Simultaneous Temperature and Mass Induced Buoyancy Driven Flmentioning
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